JPS6199560A - Method for maintaining constant outflow rate of molten metal in ladle - Google Patents

Method for maintaining constant outflow rate of molten metal in ladle

Info

Publication number
JPS6199560A
JPS6199560A JP22018184A JP22018184A JPS6199560A JP S6199560 A JPS6199560 A JP S6199560A JP 22018184 A JP22018184 A JP 22018184A JP 22018184 A JP22018184 A JP 22018184A JP S6199560 A JPS6199560 A JP S6199560A
Authority
JP
Japan
Prior art keywords
molten metal
ladle
height
outflow
detected
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP22018184A
Other languages
Japanese (ja)
Inventor
Akihisa Harada
明久 原田
Noboru Koyamatsu
小屋松 昇
Yasuo Kurachi
倉地 康夫
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Jiryoku Senko Co Ltd
Original Assignee
Nippon Jiryoku Senko Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Jiryoku Senko Co Ltd filed Critical Nippon Jiryoku Senko Co Ltd
Priority to JP22018184A priority Critical patent/JPS6199560A/en
Publication of JPS6199560A publication Critical patent/JPS6199560A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D39/00Equipment for supplying molten metal in rations
    • B22D39/06Equipment for supplying molten metal in rations having means for controlling the amount of molten metal by controlling the pressure above the molten metal

Abstract

PURPOSE:To maintain the specified outflow rate of a molten metal by evacuating the inside of a ladle when the height of the molten metal in the ladle is higher than a reference height and pressurizing the same when the height is lower than the reference height. CONSTITUTION:The optional height of the molten metal in the ladle is determined as the reference height and the height of the molten metal in the ladle during outflow is detected. The detected height and the reference height are compared and the molten metal is evacuated until both heights are made equal when the detected height is larger than the reference height. The molten metal is pressurized in the opposite case so that always specified outflow is executed. The degassing in the molten metal is executed by the evacuation.

Description

【発明の詳細な説明】 (産業上の利用分野) この発明は取鍋内の溶融金属の流出速度を一定に保つた
めの方法に関し、例えば溶融金属から直接金属粉末、金
属粒等を造るためのショノチング(sho t t i
ng)法、噴射法において用いる溶融金属を、取鍋内よ
り一定流速のもとで得ることができるようにした取鍋内
の溶融金属の流出速度を一定に保つための方法に関する
[Detailed Description of the Invention] (Industrial Application Field) This invention relates to a method for keeping the outflow rate of molten metal in a ladle constant, for example, for producing metal powder, metal particles, etc. directly from molten metal. shot t i
The present invention relates to a method for keeping the outflow rate of molten metal in a ladle constant, which enables the molten metal used in the ng) method and injection method to be obtained from the ladle at a constant flow rate.

(従来の技術) 従来、例えばショソチング(shotting)法、噴
射法により、溶融金属から製品歩留、製品品質の良い金
属粉末、金属粒等を造るための条件としては、■溶融金
属中の溶存酸素02、窒素N2、水素1{2の脱ガスを
充分に行うこと、■溶融金属の流速を一定に保つこと等
が要求されている。
(Prior art) Conventionally, the conditions for producing metal powder, metal grains, etc. with good product yield and product quality from molten metal by, for example, the shotting method or the injection method are as follows: ■ Dissolved oxygen in the molten metal. 02, nitrogen N2, and hydrogen 1{2 are required to be sufficiently degassed, and (2) the flow rate of the molten metal is kept constant.

そして、前述条件のうち溶融金属中の脱ガスは、一般的
に製鋼炉より受鋼した取鍋の段階で、真空吸上げ脱ガス
法、ガス吹込攪拌による取消脱ガス法、あるいは環流式
脱ガス法等により行われている。
Of the conditions mentioned above, degassing in the molten metal is generally carried out at the stage of the ladle receiving the steel from the steelmaking furnace, by vacuum suction degassing, cancellation degassing by gas injection and stirring, or reflux degassing. This is done by law etc.

また、前述条件のうち溶融金属の流速の一定化は、■柄
付き取鍋、小型の取鍋を用い、これを傾は滓の混入を防
ぎながら人手で流出速度を調整するようにして行われ、
また、■土瓶式取鍋を用い、これを上方よりクレーン等
で吊り下げてその高さを加減しながら、重心のやや下方
の回転軸を軸とする回転機構によりハンドル等で回転角
度を加減してその流出速度を調整するようにして行われ
ている。しかし、これらの方法では取鍋を傾ける必要が
あるため、ある程度広い場所を必要とし、また安全性の
点で問題がある。
In addition, among the above conditions, the flow rate of the molten metal is kept constant by using a ladle with a handle or a small ladle, which is tilted to prevent slag from being mixed in, and the flow rate is adjusted manually. ,
In addition, using a clay pot-style ladle, it is suspended from above using a crane, etc., and its height is adjusted, while the rotation angle is adjusted using a handle, etc. using a rotation mechanism centered on a rotation axis slightly below the center of gravity. This is done by adjusting the outflow speed. However, these methods require a certain amount of space because the ladle must be tilted, and there are also safety issues.

そこで、今日では一般的に取鍋としては、底部のノズル
にストッパーを配設し、これをハンドルで操作して前記
ノズルより溶融金属を流出させるようにした底注ぎ取鍋
が用いられている。
Therefore, today, a bottom pouring ladle is generally used as a ladle, in which a stopper is disposed in a nozzle at the bottom, and the stopper is operated by a handle to cause molten metal to flow out from the nozzle.

(発明が解決しようとする問題点) しかし、この底注ぎ取鍋の場合、 ■溶融金属の流出速度が取鍋内の溶融金属の高さによっ
て定まり、流出初期は流出速度が大きくなりすぎ、また
、流出終期は反対に小さくなりすぎるためその流量の調
整が困難である、 ■前述■のように流量の調整が困難であるため、ショソ
チング法、噴射法により溶融金属より直接一定品質の金
属粉末、金属粒等を得ようとする場合、水ジエツトスピ
ードを調整しなければならず、また、得た製品(金属粉
末、金属粒等)の歩留が悪い、 ■前述した取鍋と同様に取鍋の段階で脱ガスをする場合
、脱ガスと、溶融金属の流出とは別々の工程として行う
必要があるためこの段階における作業が複雑となる、 等の問題点がある。
(Problems to be Solved by the Invention) However, in the case of this bottom-pouring ladle, ■ The outflow speed of the molten metal is determined by the height of the molten metal in the ladle, and the outflow speed becomes too high in the initial stage of outflow. On the other hand, the flow rate becomes too small at the end of the outflow, making it difficult to adjust the flow rate. As mentioned above, it is difficult to adjust the flow rate, so metal powder of a certain quality is directly extracted from the molten metal by the shosotching method or the injection method. When trying to obtain metal particles, etc., the water jet speed must be adjusted, and the yield of the obtained products (metal powder, metal particles, etc.) is poor. When degassing is performed at the pot stage, there are problems such as the fact that degassing and flowing out of molten metal must be performed as separate processes, making the work at this stage complicated.

この発明は、以上のような点に鑑みてなしたもので、特
に底注ぎ取鍋において溶融金属の流出初期、終期にかか
わりなく一定の流出速度で溶融金属の流出を行え、しか
も並行して溶融金属内の脱ガスも行える取鍋内の溶融金
属の流出速度を一定に保つための方法を従供したもので
ある。
This invention was made in view of the above points, and it is possible to flow out molten metal at a constant flow rate regardless of the initial and final stages of the flow of molten metal, especially in a bottom pouring ladle. A method is provided for maintaining a constant outflow rate of molten metal in a ladle, which also allows for degassing within the metal.

(問題点を解決するための手段) そして、前述した問題点を解決するこの発明は取鍋内の
溶融金属の任意高さを基準高さとし、前記溶融金属の高
さが前記基準高さより高い場合は前記取鍋内を減圧し、
また前記溶融金属の高さが前記基準高さより低い場合は
前記取鍋内を加圧することにより溶融金属の流出速度を
一定に保てるようにした手段よりなるものである。
(Means for Solving the Problems) This invention that solves the above-mentioned problems uses an arbitrary height of the molten metal in the ladle as a reference height, and when the height of the molten metal is higher than the reference height, reduces the pressure inside the ladle,
Further, when the height of the molten metal is lower than the reference height, the inside of the ladle is pressurized to keep the flow rate of the molten metal constant.

ここで、取鍋としては底注ぎ取鍋を主として用いるが他
の構成の取鍋を用いてもよく、また、ここでいう取鍋と
は広い概念で溶融金属を受けるための容器全体をいい、
例えば湯だまり等であってもよい。
Here, as the ladle, a bottom pouring ladle is mainly used, but ladles of other configurations may also be used, and the ladle here refers to the entire container for receiving molten metal in a broad concept.
For example, it may be a pool of hot water.

また、溶融金属の任意高さを基準高さとするのは、溶融
金属の流出速度がベルヌーイの定理より取鍋内の溶融金
属の高さによって定まるのからであるが、溶融金属の任
意高さを基準高さとするということは任意の流出速度を
基準速度とするということでもある。
Furthermore, the reason why the arbitrary height of the molten metal is used as the reference height is that the outflow velocity of the molten metal is determined by the height of the molten metal in the ladle according to Bernoulli's theorem. Setting the reference height also means setting an arbitrary outflow velocity as the reference velocity.

そして、取鍋内の溶融金属の高さは一般的には機械的、
電気的手段によって検出されるが、検出しようとする高
さHにおける溶融金属の流出速度V(粘性を考慮してい
ない)が、 v = Cv7丁7π ここで、Cvは速度係数 で得られ、単位時間ごとの溶融金属のノズルよりの流出
量Qが、 q−caAh7丁 ここで、C4は流出係数 Aはノズルの断面積 で得られることより流出速度または/および流出量を検
出して溶融金属の高さを得るようにしてもよい。
And the height of molten metal in the ladle is generally determined mechanically,
Although it is detected by electrical means, the outflow velocity V (not taking into account viscosity) of the molten metal at the height H to be detected is v = Cv7d7π where Cv is obtained by the velocity coefficient and has the unit The flow rate Q of molten metal from the nozzle per hour is q-caAh7 where C4 is the flow coefficient A is obtained from the cross-sectional area of the nozzle. It may also be possible to obtain the height.

この場合、基準速度と検出速度とを比較し、間接的に溶
融金属の任意高さと検出高さとを比較するという形態を
とることになる。
In this case, the reference speed and the detected speed are compared, and the arbitrary height of the molten metal and the detected height are indirectly compared.

また、減圧、加圧は一般的手段で行い、取鍋内の変化す
る溶融金属の高さに応じて時系列的に変化させて行う。
Further, the pressure reduction and pressurization are carried out by general means, and are carried out by changing the pressure in a time-series manner according to the changing height of the molten metal in the ladle.

すなわち、溶融金属の検出高さに応じて順次連続的、あ
るいは断続的に変化させるようにして行う。
That is, the height is changed continuously or intermittently depending on the detected height of the molten metal.

(作用) つぎに、以上の構成に基づいてこの発明の作用について
説明する。
(Operation) Next, the operation of the present invention will be explained based on the above configuration.

取鍋内の溶融金属の任意高さを基準筒さとし、流出中の
溶融金属の取鍋内の高さを検出し、検出高さと任意高さ
を比較し、検出高さが基準高さより大きい場合はその高
さが等しくなるまで減圧し、逆の状態となった場合は加
圧を行い、常に一定(はぼ)の流出を行えるように作用
するとともに、前記減圧により溶融金属内の脱ガスを行
うように作用する。
The arbitrary height of the molten metal in the ladle is used as a reference cylinder, the height of the flowing molten metal inside the ladle is detected, the detected height and the arbitrary height are compared, and if the detected height is greater than the reference height The pressure is reduced until the heights are equal, and if the situation is reversed, the pressure is increased to ensure a constant outflow at all times. act to do.

(実施例) 以下、ショッチング法、噴射法により溶融金属j   
  から直接金属粒(ショツト粒)を造る場合について
の実施例に基づき、この発明をより具体的に説明する。
(Example) Hereinafter, molten metal j
The present invention will be explained in more detail based on an example in which metal grains (shot grains) are directly produced from.

まづ、取鍋として底注ぎ取鍋を用いる。そして、あらか
じめこの底注ぎ取鍋による溶融金属の高さと流出速度と
の関係を理論値あるいは実験値(溶融金属の場合、水と
異なり比重が比較的高いため粘性を考慮しなければなら
ないので通常は実験値)で知っておき、取鍋内の溶融金
属の任意高さを基準高さとして設定する。
First, use a bottom pouring ladle as the ladle. The relationship between the height of the molten metal and the outflow velocity from the bottom pouring ladle is determined in advance by either theoretical or experimental values (in the case of molten metal, unlike water, its specific gravity is relatively high, so viscosity must be taken into account, so (experimental value) and set the arbitrary height of the molten metal in the ladle as the reference height.

次いで、電気炉等より取鍋内に出鋼した溶融金属をノズ
ルより連続的に流出するとともに水ジェツトにより水中
に噴射して金属粒(ショツト粒)を得る。ここで、前記
溶融金属の流出にあたっては、取鍋内の溶融金属の高さ
を検出し、検出高さと基準高さを比較し、検出高さが基
準高さより大きい場合はその高さが等しくなるまで減圧
し、減圧により溶融金属内に溶存する酸素0□、窒素N
2、水素H2の脱ガスをしながら行い流出速度を調整す
る。
Next, the molten metal tapped into the ladle from an electric furnace or the like is continuously flowed out from a nozzle and sprayed into water by a water jet to obtain metal grains (shot grains). Here, when the molten metal flows out, the height of the molten metal in the ladle is detected, the detected height and the reference height are compared, and if the detected height is greater than the reference height, the heights are equal. The pressure is reduced to 0□ oxygen and nitrogen N dissolved in the molten metal due to the reduced pressure.
2. Adjust the outflow rate while degassing hydrogen H2.

つづいて、取鍋内の溶融金属の高さを検出し、検出高さ
と基準高さを比較し、検出高さが基準高さより小さくな
ると逆に取鍋内を加圧し、溶融金属の流出速度を調整し
、所定の溶融金属を全部流出して金属粒(ショット粒)
を得る。ここで、加圧をしているがこれによる脱ガスに
対しての悪影響はみられなかった。
Next, the height of the molten metal in the ladle is detected, the detected height is compared with the reference height, and when the detected height is smaller than the reference height, the inside of the ladle is pressurized and the flow rate of the molten metal is reduced. After adjusting, all the specified molten metal flows out and becomes metal particles (shot particles).
get. Although pressurization was applied here, no adverse effect on degassing was observed.

そして、この実施例によれば必要な金属粒(ショツト粒
)サイズを歩留よ(得ることができる。
According to this embodiment, the required size of metal grains (shot grains) can be obtained in yield.

−実験例− 以上の実施例に基づいて、つぎの条件のもとて実験を行
いその効果を確認した。
-Experimental Example- Based on the above examples, experiments were conducted under the following conditions to confirm the effects.

内径0.8m、高さ2.50m、流出孔の内径0.01
8mの底注ぎ取鍋を用い、温度1500℃、炭素Cの含
有率0.8%、比重7.0の溶融金属について、取鍋内
の熔融金属の基準高さを0.75mとして実験した。
Inner diameter 0.8m, height 2.50m, inner diameter of outflow hole 0.01
Using an 8 m bottom pouring ladle, an experiment was conducted on molten metal at a temperature of 1500° C., a carbon C content of 0.8%, and a specific gravity of 7.0, with the standard height of the molten metal in the ladle being 0.75 m.

そして、その結果は第1表のとおりである。The results are shown in Table 1.

−比較例− また、実験例の結果と比較してその効果を確認するため
に前記実験例と同じ条件のもとで、従来の手段(圧力調
整をせず)で行った。
- Comparative Example - In addition, in order to confirm the effect by comparing with the results of the experimental example, a conventional method (without pressure adjustment) was conducted under the same conditions as the experimental example.

そして、その結果は第2表のとおりである。The results are shown in Table 2.

第1表 ※1・・溶融金属の高さ 第2表 f また、以上の実験例と比較例との関連を明確にするため
に調整圧力(mmHg )と溶融金属の高さくm)との
関係を表すグラフを第1図に、また溶融金属の流出速度
(m/s)と溶融金属の高さくm)との関係を表すグラ
フを第2図に示した。
Table 1 *1 Height of molten metal Table 2 f Also, to clarify the relationship between the above experimental examples and comparative examples, we also show the relationship between the adjusted pressure (mmHg) and the height of molten metal (m). A graph showing the relationship between the outflow velocity (m/s) of the molten metal and the height (m) of the molten metal is shown in FIG. 2.

−製品歩留の比較− さらに、実施例の効果を確認するために、前述実験例と
比較例とに基づき、金属粒(ショット粒サイズ:2.8
3〜0.297mmについての製品歩留の比較を行った
-Comparison of product yield- Furthermore, in order to confirm the effects of the examples, metal particles (shot particle size: 2.8
A comparison of product yields was made for 3 to 0.297 mm.

そして、その結果は第3表のとおりである。The results are shown in Table 3.

第3表 一製品品質の比較− さらに、実施例の効果を確認するために、前述実験例と
比較例とに基づき、ライフテストと研掃カテストとによ
り製品品質の比較を行った。   ・〔ライフテストに
よる比較〕 投射スピード二80%、残留率:45%(55%ブレー
クダウン法)のテスト条件でライフテストにより製品品
質(投射回数)の比較を行った。
Table 3 - Comparison of product quality - Further, in order to confirm the effects of the examples, product quality was compared using a life test and a cleaning force test based on the above-mentioned experimental example and comparative example. - [Comparison by Life Test] Product quality (number of shots) was compared by a life test under test conditions of 80% projection speed and 45% residual rate (55% breakdown method).

そして、その結果は第4表のとおりである。The results are shown in Table 4.

第4表   (投射回数) ※l・・溶融金属の高さ なお、5240.5140はJIS G 5903によ
る粒度である。
Table 4 (Number of projections) *l...Height of molten metal Note that 5240.5140 is the particle size according to JIS G 5903.

〔研掃カテストによる比較〕[Comparison by grinding test]

投射スピード: 67m/s投射密度: 90kg/m
2テストピース:5S41のテスト条件で研掃カテスト
により製品品質の比較を行った。そして、その結果は第
5表のとおりである。
Projection speed: 67m/s Projection density: 90kg/m
2 test pieces: Comparison of product quality was conducted by abrasive test under test conditions of 5S41. The results are shown in Table 5.

第5表 Rz表面粗さくμm) ※1・・熔融金属の高さ なお、Rz  (10点平均粗さ)はJIS B 06
01による。
Table 5 Rz surface roughness (μm) *1: Height of molten metal. Rz (10 point average roughness) is JIS B 06
According to 01.

そして、以上の実験例、比較例、実験例と比較例とに基
づく製品歩留δよび製品品質の比較による成績結果より
実施例の手段について、次のことが確認できた。
From the results of comparisons of product yield δ and product quality based on the above experimental examples, comparative examples, experimental examples and comparative examples, the following was confirmed regarding the means of the examples.

■溶融金属の減圧・加圧によりその流出速度をほぼ一定
化することができる。これは、比較例の場合、流出孔に
かかる溶融金属の圧力差のためで、実験例の場合、この
圧力差を充分に調整できたからである。また、この点は
第2図に示すグラフより確認できる。
■By reducing or pressurizing the molten metal, the flow rate can be made almost constant. This is because, in the case of the comparative example, there is a pressure difference in the molten metal applied to the outflow hole, and in the case of the experimental example, this pressure difference can be sufficiently adjusted. Moreover, this point can be confirmed from the graph shown in FIG.

■流出速度の一定化と同時に溶融金属内の脱ガス処理が
充分に行える。すなわち、溶融金属内に溶存する酸素0
2、窒素N2、水素11□の脱ガス処理ができる。この
点は製品(実験例ではショツト粒)のライフが延長でき
、しかもショツト粒としての研掃力が増加し、その品質
が向上したことより確認できた(第4.5表参照)。こ
れに対して比較例、      +7)場合・別1程7
脱ガ3処理をじけ0ば4ら4いという点がある。また、
実験例のものについても別工程で更に脱ガスをしたもの
については一層の品質の向上が認められる。なお、実験
例、比較例ともにここでは別工程で脱ガス処理をしてい
ない。
■At the same time as keeping the outflow rate constant, degassing inside the molten metal can be sufficiently performed. In other words, 0 oxygen dissolved in the molten metal
2. Capable of degassing nitrogen N2 and hydrogen 11□. This point was confirmed by the fact that the life of the product (shot granules in the experimental example) was extended, the abrasive power of the shot granules increased, and the quality improved (see Table 4.5). On the other hand, comparative example, +7) Case/Another 1 degree 7
There is a point that it is difficult to stop the degassing process. Also,
Regarding the experimental samples, further improvement in quality was observed when the samples were further degassed in a separate process. In addition, in both the experimental example and the comparative example, degassing treatment was not performed in a separate process.

■異形、低比重の製品があまりみられず、製品歩留の向
上が認められる(第3表参照)。また、水蒸気爆発の危
険がなくなり安全性が向上し、さらに、廃熱をショツト
粒の乾燥に利用できることが確認できた。
■Products with irregular shapes and low specific gravity are not often seen, and an improvement in product yield is observed (see Table 3). In addition, it was confirmed that the danger of steam explosion was eliminated, improving safety, and that waste heat could be used to dry short grains.

なお、以上の実施例は、ショノチング法、噴射法により
溶融金属から直接金属粒(ショット粒)を造る場合につ
いてであるが、鋳物の鋳込等にも通用できるものである
ことはいうまでもない。
The above examples are for the case where metal grains (shot grains) are made directly from molten metal by the shotting method or injection method, but it goes without saying that the method can also be applied to casting of castings, etc. .

また、ここでは、減圧・加圧について第1図に示すよう
に溶融金属の高さの関数として直線的に変化させたが、
これは取鍋の形状等によって変えることは当然である。
In addition, here, as shown in Figure 1, the pressure reduction and pressure were changed linearly as a function of the height of the molten metal.
Naturally, this may vary depending on the shape of the ladle, etc.

(発明の効果) 以上の記載より明らかなように、この発明によれば、取
鍋よりの溶融金属の流出初期、終期にかかわりなく一定
の流出速度で溶融金属の流出を行え、しかも並行して溶
融金属内の脱ガスも行える取鍋内の溶融金属の流出速度
を一定に保つための方法を提供することができる。
(Effects of the Invention) As is clear from the above description, according to the present invention, the molten metal can be flowed out at a constant flow rate regardless of the initial and final stages of the flow of the molten metal from the ladle, and moreover, the molten metal can be flowed out in parallel. A method can be provided for maintaining a constant outflow rate of molten metal in a ladle that also allows for degassing within the molten metal.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はこの発明の実施例における調整圧力(mmHg
 )と溶融金属の高さく’m)との関係を表すグラフ、
第2図はこの発明の実施例における溶融金属の流出速度
(m/s)と溶融金属の高さくm)との関係を表すグラ
フである。 第1図 第2図
FIG. 1 shows the adjusted pressure (mmHg) in an embodiment of this invention.
) and the height of molten metal 'm),
FIG. 2 is a graph showing the relationship between the outflow velocity (m/s) of molten metal and the height (m) of molten metal in an embodiment of the present invention. Figure 1 Figure 2

Claims (3)

【特許請求の範囲】[Claims] (1)取鍋内の溶融金属の任意高さを基準高さとし、前
記溶融金属の高さが前記基準高さより高い場合は前記取
鍋内を減圧し、また前記溶融金属の高さが前記基準高さ
より低い場合は前記取鍋内を加圧することにより溶融金
属の流出速度を一定に保てるようにしたことを特徴とす
る取鍋内の溶融金属の流出速度を一定に保つための方法
(1) An arbitrary height of the molten metal in the ladle is set as the reference height, and when the height of the molten metal is higher than the reference height, the pressure inside the ladle is reduced, and the height of the molten metal is set as the reference height. A method for maintaining a constant outflow rate of molten metal in a ladle, characterized in that the outflow rate of molten metal in a ladle is kept constant by pressurizing the inside of the ladle when the outflow rate is lower than the height of the ladle.
(2)減圧量または加圧量を取鍋内の溶融金属の高さに
応じて時系列的に変化させることにより、取鍋内の溶融
金属の定量流出が行えるようにしたたことを特徴とする
前記特許請求の範囲(1)に記載の取鍋内の溶融金属の
流出速度を一定に保つための方法。
(2) The feature is that the molten metal in the ladle can be flowed out in a fixed amount by changing the amount of pressure reduction or the amount of pressurization in time series according to the height of the molten metal in the ladle. A method for maintaining a constant flow rate of molten metal in a ladle according to claim 1.
(3)取鍋として底注ぎ取鍋を用いるようにしたことを
特徴とする前記特許請求の範囲(1)または(2)に記
載の取鍋内の溶融金属の流出速度を一定に保つための方
法。
(3) A method for keeping the flow rate of molten metal in the ladle constant according to claim (1) or (2), characterized in that a bottom pouring ladle is used as the ladle. Method.
JP22018184A 1984-10-18 1984-10-18 Method for maintaining constant outflow rate of molten metal in ladle Pending JPS6199560A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22018184A JPS6199560A (en) 1984-10-18 1984-10-18 Method for maintaining constant outflow rate of molten metal in ladle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22018184A JPS6199560A (en) 1984-10-18 1984-10-18 Method for maintaining constant outflow rate of molten metal in ladle

Publications (1)

Publication Number Publication Date
JPS6199560A true JPS6199560A (en) 1986-05-17

Family

ID=16747150

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22018184A Pending JPS6199560A (en) 1984-10-18 1984-10-18 Method for maintaining constant outflow rate of molten metal in ladle

Country Status (1)

Country Link
JP (1) JPS6199560A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5776107A (en) * 1980-06-30 1982-05-13 Leybold Heraeus Gmbh & Co Kg Metal powder manufacturing device from metal melt
JPS5779102A (en) * 1980-09-08 1982-05-18 Asea Ab Metal powder producing method and device
JPS6024304A (en) * 1983-07-19 1985-02-07 Hitachi Metals Ltd Device for producing alloy powder

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5776107A (en) * 1980-06-30 1982-05-13 Leybold Heraeus Gmbh & Co Kg Metal powder manufacturing device from metal melt
JPS5779102A (en) * 1980-09-08 1982-05-18 Asea Ab Metal powder producing method and device
JPS6024304A (en) * 1983-07-19 1985-02-07 Hitachi Metals Ltd Device for producing alloy powder

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